WO2012015308A1 - Aqueous slurry of amorphous silica and method for its production - Google Patents
Aqueous slurry of amorphous silica and method for its production Download PDFInfo
- Publication number
- WO2012015308A1 WO2012015308A1 PCT/NO2011/000151 NO2011000151W WO2012015308A1 WO 2012015308 A1 WO2012015308 A1 WO 2012015308A1 NO 2011000151 W NO2011000151 W NO 2011000151W WO 2012015308 A1 WO2012015308 A1 WO 2012015308A1
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- WO
- WIPO (PCT)
- Prior art keywords
- slurry
- sepiolite
- silica
- amorphous silica
- range
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B14/00—Use of inorganic materials as fillers, e.g. pigments, for mortars, concrete or artificial stone; Treatment of inorganic materials specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B14/02—Granular materials, e.g. microballoons
- C04B14/04—Silica-rich materials; Silicates
- C04B14/041—Aluminium silicates other than clay
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/18—Preparation of finely divided silica neither in sol nor in gel form; After-treatment thereof
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/04—Waste materials; Refuse
- C04B18/14—Waste materials; Refuse from metallurgical processes
- C04B18/146—Silica fume
- C04B18/147—Conditioning
- C04B18/148—Preparing silica fume slurries or suspensions
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/02—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B40/00—Processes, in general, for influencing or modifying the properties of mortars, concrete or artificial stone compositions, e.g. their setting or hardening ability
- C04B40/0028—Aspects relating to the mixing step of the mortar preparation
- C04B40/0039—Premixtures of ingredients
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/42—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells
- C09K8/46—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells containing inorganic binders, e.g. Portland cement
- C09K8/467—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells containing inorganic binders, e.g. Portland cement containing additives for specific purposes
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2103/00—Function or property of ingredients for mortars, concrete or artificial stone
- C04B2103/0027—Standardised cement types
- C04B2103/0028—Standardised cement types according to API
- C04B2103/0035—Type G
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Definitions
- the present invention relates to an aqueous slurry of microsilica, optionally including silica flour, and to a method for producing such a slurry.
- microsilica refers to particulate, amorphous SiO 2 obtained from a process in which silica (quartz) is reduced to SiO-gas and the reduction product is oxidised in the vapour phase to form amorphous silica.
- Microsilica may contain at least 70% by weight silica (SiO 2 ), and preferably >97% and has a specific density of 2.1 - 2.3g/cm 3 and a surface area of 12 - 40m 2 /g, typically 20m 2 /g.
- the primary particles are substantially spherical and may have an average size of about 0.15 ⁇ .
- Microsilica is preferably obtained as a co- product in the production of silicon alloys in electric reduction furnaces.
- Microsilica slurry is currently used widely in construction applications such as fibre cement, concrete and in oil well cementing. Microsilica acts as pozzolanic material or inorganic binder by interacting with calcium hydroxide as a hydration product of Portland cement and water to improve the
- microsilica used in slurry form performs much better than in powder form.
- Most commercially available microsilica slurries are normally supplied as 50 wt% microsilica slurries.
- Sulphuric acid is normally used to adjust the pH of the dispersion to lie in the range 4 to 7, to give stability to the dispersion.
- Conventional microsilica slurry suffers from two challenges, namely, geletion and settling.
- microsilica slurry in terms of sedimentation and geletion depends mainly on the quality of the dry microsilica used for making the slurry. Since microsilica has a very small particle size, a slurry will show a high stability towards sedimentation when stored for long periods of time; more than 3 months for a well-dispersed slurry. However, when considering the stability of a microsilica slurry, a distinction should be made between particle settling and geletion.
- Settling is a natural phenomenon for many inorganic dispersions such as silica, alumina or titania. According to Stoke 's low, the main factors affecting settling are the low apparent viscosity of the continuous phase (water) and the size of the dispersed particles. The larger the dispersed particles, the faster the settling rate will be. Generally, a 50 wt% silica slurry with a SiO 2 content >95 wt% has a high potential for settling due to the low apparent viscosity of ⁇ 20mPa.s at a shear rate of 20s "1 . Settling of coarse particles can be avoided by sieving the slurry or by increasing the viscosity of slurry by employing thickening agents such as Xanthen gum, cellulose, polyacrylate or nanosilica.
- thickening agents such as Xanthen gum, cellulose, polyacrylate or nanosilica.
- Geletion or network formation by the particles occurs when the particles are attracted to each other due to Van der Waals forces and/or chemical bridging by cations, creating a network structure which can have different forms and strengths.
- the main factor influencing geletion in the case of a microsilica slurry is contamination with other inorganic metal oxides such as K 2 O, Na 2 0, CaO, MgO, Al 2 O 3 and Fe 2 O 3 These oxides occur naturally in microsilica and dissolve to a certain extent into the water, providing the aqueous phase with different types of cations which tend to make bridges between the particles.
- the bridging causes the microsilica particles to agglomerated or flocculate which results in a high viscosity and even gel or paste formation in some cases.
- microsilica can be classified into three types according to the tendency to form a gel: a) Not forming a gel would be microsilica with a total metal oxide (TMO) below 3 wt%.
- TMO total metal oxide
- Microsilica forming a gel (network) would be microsilica with a TMO larger than 3 wt%.
- Microsilica forming a hard gel (network) would be with a TMO larger than 10 wt%.
- an aqueous slurry of amorphous silica the amorphous silica having a particle size less than 1 ⁇ , characterised in that the slurry contains sepiolite as a stabiliser.
- sepiolite a hydrated magnesium silicate
- Pangel S9, Pangel HV and Pangel SI 500 are proprietary types of sepiolite, supplied by Tolsa, Spain.
- the sepiolite is present as 0.1 to 1% by weight of the slurry, more preferably as 0.2 to 0.5% by weight of the slurry.
- the slurry has a solids content in the range 40 to 80 wt% of the slurry, preferably about 50 wt%.
- the slurry may also comprise silica flour, in addition to the amorphous silica.
- the slurry may contain varying amounts of amorphous silica and silica flour, but the amount of amorphous silica is generally between 15 - 50% by weight based on the weight of the slurry and the amount of silica flour is generally between 30 and 60% by weight based on the weight of the slurry.
- the silica flour has a particle size in the range 2 to 200 ⁇ .
- the silica flour constitutes up to 65wt% of the total solids content of the slurry.
- a method for the production of an aqueous slurry containing water and amorphous silica having a particle size less than ⁇ characterised in that sepiolite is included in the slurry as a stabiliser.
- a high shear mixer is used to prepare the slurry initially, and to mix in any additional components.
- the sepiolite is hydrated with water and is then added to the slurry of water and amorphous silica, and mixed to form a stabilised slurry.
- the pH of the slurry is adjusted to a value in the range 4 to 7.
- Bentonite is aluminosilicate clay with a plate structure. Bentonite presents strong colloidal properties and its volume increases several times when coming into contact with water, creating a gelatinous and viscous fluid.
- the special properties of bentonite hydro, swelling, water absorption, viscosity and thixotropy make it a valuable material for a wide range of uses and
- bentonite tends to form hard gel over time even when using low dosages. Therefore, bentonite is not a suitable stabiliser for the amorphous silica slurry.
- Pangel HV and Pangel S9 were relatively difficult to disperse in the slurry compared to Pangel SI 500. No hydration time was required in the case of the sepiolite, though hydration time was necessary for bentonite and the biopolymer tested below. Table 2: Properties of Pangel products tested
- the optimal concentration fro Pangel SI 500 to stabilise the 50 wt% slurry lies in the range of 2 to 5g/kg slurry.
- Pangel HV Tests were also made with Pangel HV. 5 grams of Pangel HV was added to a 50 wt % microsilica slurry from Elkem Bremanger. The mixing speed of the warring blender was varied between 4000 and
- microsilica slurry containing Pangel HV 5g/kg slurry.
- Table 4 Effect of mixing time on the viscosity of MS slurry containing Pangel HV with a concentration of lOg/kg slurry.
- Figure 4 shows the viscosity of the slurry stabilised with xanthan gum as a function of xanthan gum concentration.
- Colloidal silica is amorphous silica particles with a size in the range 5 - lOOnm dispersed in water with a solid load in the range from 15 to 50 wt%.
- the typical pH range is from 9 - 11.
- Colloidal silica is produced via cationic exchange with sodium silicate at the desired pH, where the polymerization takes place. The sol is stabilised by pH adjustment and concentrated to the desired content.
- the surface of colloidal silica like many other silica particles consists mainly of hydroxyl groups, or -Si-O-H, though other groups such as silandiol, -Si-(OH) 2 , silanetriol, -Si(OH) 3 , surface siloxanes, -Si-O-Si-O-, and surface-bound water may also be present.
- the surface of colloidal silica is anionic in an alkaline medium. It is stabilised with cations such as sodium or ammonium. In the case of cationic sols, polyaluminum chloride can be used as stabilising agent. Two colloidal silica, Cembinder 45 and 50, supplied by Eka Chemicals AB, Sweden, were used in this study. The properties are set out in Table 6.
- Table 6 Properties of Cembinder 45 and 50 from Eka Chemicals AB.
- the first set of experiments with Cembinder as stabiliser for the slurry was conducted at different levels of concentration of Cembinder 45 ranging from 2.5 to 25g dry silica/kg slurry.
- Cembinder 45, with a solid loading of 33 wt% was added as slurry into an amorphous silica slurry with solid loading of 60 wt%.
- the solid loading in all the experiments was adjusted to 50 wt% by adding water.
- the viscosity of the slurry increases exponentially as function of Cembinder 45 concentration. Oscillation measurements showed that a network structure only built above a certain Cembinder concentration level of 5g/kg slurry.
- Cembinder 50 is a silica suspension with a solid loading of 17 wt% and a pH of 10. The average particle size is assumed to be below 40 nm and it was not measurable by the Malvern method due to the weak light scattering signal. As with Cembinder 45, the viscosity of the slurry doped with Cembinder 50 increases with the time. At concentrations of 5g/kg slurry, Cembinder 45 formed a hard gel over time. This viscosity increase over time is shown in Figure 7.
- the chemical structure consists of beta-l,3-D-glucose backbones with one beta-l,6-D- glucose side chain every three main backbone. Dissolved Scleroglucan chains form a rod-like triple helical structure, in which the glucose backbones are on the outside, thus preventing the helices from coming close to each other and aggregating.
- Scleroglucan molecules are in a single chain random coil state when the pH is greater than
- the viscosity of the slurry stabilised with Scleroglucan as a function of the Scleroglucan is shown in Figure 8.
- a gel structure starts to be formed at a concentration level >2g/kg slurry.
- the viscosity was very dependent on pH, particularly above 6 which is undesirable.
- the viscosity changes over time.
- Figure 9 shows a comparison of the rheology of the slurry stabilised by the different stabilisers.
- Sepiolite shows the highest low shear rheology which makes it a good candidate for this application.
- the shear thinning properties of the sepiolite stabilised slurry indicates a weak network structure that is easily breakable by applying low shear energy. This is an important requirement, namely, a non-settleable and easily pourable slurry.
- Pangel 1500S is the best additive to avoid the sedimentation of an amorphous silica slurry.
- a concentration level of 5g/kg slurry showed good stability for 6 months.
- the following formulation gave good, stable slurry;
- Castament FS20 is a dispersing agent used to weaken the effect of cationic species in the aqueous phase that are responsible for gel information
- Example 6 compares the performance of sepiolite with xanthan gum as a stabiliser for an aqueous slurry of amorphous silica and silica flour.
- XC polymer P is a powder polymer for received from Jungbunzlauer and XC polymer is a liquid polymer received from CP Kelco Oil Field Group.
- the xanthan gum concentration in the both tests was 0.072g/kg slurry.
- compositions using three different amounts of sepiolite clay were compositions using three different amounts of sepiolite clay.
- the sepiolite used was Pangel S9.
- the three sepiolite-containing compositions were made up as follows:
- SEP Bl 24g were added to 976g of a 50 wt% aqueous slurry of amorphous silica and mixed to form SEP B2
- SEP CI 18g of SEP CI were added to 982g of 50 wt% aqueous slurry of amorphous silica and mixed to form SEP C2
- silica flour (Sibelco M10) were added to 800g of each of the slurries SEP A2, SEP B2 and SEP C2 and then mixed to form, respectively, SEP A3, SEP B3 and SEP C3.
- the pH of these slurries was adjusted to pH5 using sulphuric acid.
- the plastic viscosity of the sepiolite slurries was less by 3 magnitudes than the plastic compared to viscosity of the slurries with xanthan gum.
- the yield points were also less compared to the xanthan gum slurries.
- Pangel SI 500 The optimal dosage of Pangel SI 500 was determined after many lab trials, to lie in the range of 2 - lOg/kg slurry. Below that range settling of silica flour tends to take place. Above that range the slurry tends to form an undesirable gel over time. The optimal clay dosage is 3.5g/kg slurry. This gives enough stability and a low production cost. Adding the clay before or after silica flour has no effect on the product rheology and consequently on the product stability.
- silica slurry according to the invention stabilized by sepiolite was tested in an oil well cement with a density of 1.9kg/m 3 and compared with similar slurry stabilized by xanthan gum.
- the cement test was conducted according to the API 10 standard.
- the recipe shown in Table 7 was used to prepare cement slurries with a density of 1.9 kg/ m 3 .
- Table 7 Recipe of oil well cement containing an aqueous slurry of amorphous silica and silica flour.
- Antifoam agent 0.9 The following equipment were used to prepare and characterize the cement slurries:
- Table 8 Rheology and fluid loss of cement slurry using two different silica slurries.
- the compressive strength measured by ultrasonic technique showed interesting results.
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- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Inorganic Chemistry (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Civil Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Silicon Compounds (AREA)
- Colloid Chemistry (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR112012030670-7A BR112012030670B1 (en) | 2010-07-26 | 2011-05-16 | WATER FLUID PASTE OF AMORPHAL SILICA, AND, METHOD FOR THE PRODUCTION OF WATER FLUID PASTE |
CA2802512A CA2802512C (en) | 2010-07-26 | 2011-05-16 | Aqueous slurry of amorphous silica and method for its production |
EP11812822.2A EP2598457B1 (en) | 2010-07-26 | 2011-05-16 | Aqueous slurry of amorphous silica and method for its production |
ES11812822.2T ES2566955T3 (en) | 2010-07-26 | 2011-05-16 | Aqueous suspension of amorphous silica and method for its production |
DK11812822.2T DK2598457T3 (en) | 2010-07-26 | 2011-05-16 | DIFFICULT SUSPENSION OF AMORF SILICA AND PROCEDURES FOR PREPARING IT |
US13/811,850 US8585819B2 (en) | 2010-07-26 | 2011-05-16 | Aqueous slurry of amorphous silica and method for its production |
MX2012015041A MX340657B (en) | 2010-07-26 | 2011-05-16 | Aqueous slurry of amorphous silica and method for its production. |
EA201390164A EA022621B1 (en) | 2010-07-26 | 2011-05-16 | Aqueous slurry of amorphous silica and method for its production |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NO20101066A NO334511B1 (en) | 2010-07-26 | 2010-07-26 | Aqueous slurry of amorphous silica and process for making such slurry |
NO20101066 | 2010-07-26 |
Publications (1)
Publication Number | Publication Date |
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WO2012015308A1 true WO2012015308A1 (en) | 2012-02-02 |
Family
ID=45530324
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/NO2011/000151 WO2012015308A1 (en) | 2010-07-26 | 2011-05-16 | Aqueous slurry of amorphous silica and method for its production |
Country Status (11)
Country | Link |
---|---|
US (1) | US8585819B2 (en) |
EP (1) | EP2598457B1 (en) |
BR (1) | BR112012030670B1 (en) |
CA (1) | CA2802512C (en) |
DK (1) | DK2598457T3 (en) |
EA (1) | EA022621B1 (en) |
ES (1) | ES2566955T3 (en) |
MX (1) | MX340657B (en) |
NO (1) | NO334511B1 (en) |
PL (1) | PL2598457T3 (en) |
WO (1) | WO2012015308A1 (en) |
Cited By (5)
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CN102775972A (en) * | 2012-07-16 | 2012-11-14 | 中国海洋石油总公司 | Liquid high-temperature resistant declining agent for well cementation and preparation method thereof |
CN105255462A (en) * | 2015-09-02 | 2016-01-20 | 南京云越新材料科技有限公司 | Liquid silicon and preparation method thereof |
WO2018052307A1 (en) * | 2016-09-13 | 2018-03-22 | Elkem As | Microsilica slurry and method for producing such slurry |
CN110467384A (en) * | 2019-09-10 | 2019-11-19 | 宋文奇 | A kind of light-high-strength concrete and preparation method thereof |
US11021399B2 (en) | 2019-01-23 | 2021-06-01 | United States Gypsum Company | Self-consolidating geopolymer compositions and methods for making same |
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BR112016029652A2 (en) | 2014-08-05 | 2017-08-22 | Halliburton Energy Services Inc | drilling method and drilling fluid |
US10030187B2 (en) | 2014-08-05 | 2018-07-24 | Halliburton Energy Services, Inc. | Polymer-based drilling fluids containing non-biodegradable particulates and methods for use thereof |
US9624131B1 (en) | 2015-10-22 | 2017-04-18 | United States Gypsum Company | Freeze-thaw durable geopolymer compositions and methods for making same |
KR20200128572A (en) | 2018-03-09 | 2020-11-13 | 더스틴 에이. 하트만 | Novel composition for improved concrete performance |
JP7344272B2 (en) | 2018-03-22 | 2023-09-13 | ダスティン エイ ハートマン | Method for preparing improved finished concrete products |
US20200039884A1 (en) | 2018-08-03 | 2020-02-06 | United States Gypsum Company | Geopolymer compositions and methods for making same |
US11459500B2 (en) * | 2018-09-17 | 2022-10-04 | Halliburton Energy Services, Inc. | Foamed treatment fluids comprising nanoparticles |
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US11447681B2 (en) | 2019-07-30 | 2022-09-20 | Halliburton Energy Services, Inc. | Aqueous silica dispersion |
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CN112569877B (en) * | 2020-12-10 | 2023-02-10 | 苏州中材非金属矿工业设计研究院有限公司 | Modified bentonite inorganic gel and preparation method and application thereof |
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2010
- 2010-07-26 NO NO20101066A patent/NO334511B1/en not_active IP Right Cessation
-
2011
- 2011-05-16 WO PCT/NO2011/000151 patent/WO2012015308A1/en active Application Filing
- 2011-05-16 US US13/811,850 patent/US8585819B2/en active Active
- 2011-05-16 EA EA201390164A patent/EA022621B1/en unknown
- 2011-05-16 ES ES11812822.2T patent/ES2566955T3/en active Active
- 2011-05-16 DK DK11812822.2T patent/DK2598457T3/en active
- 2011-05-16 EP EP11812822.2A patent/EP2598457B1/en active Active
- 2011-05-16 BR BR112012030670-7A patent/BR112012030670B1/en not_active IP Right Cessation
- 2011-05-16 MX MX2012015041A patent/MX340657B/en active IP Right Grant
- 2011-05-16 CA CA2802512A patent/CA2802512C/en not_active Expired - Fee Related
- 2011-05-16 PL PL11812822.2T patent/PL2598457T3/en unknown
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102775972A (en) * | 2012-07-16 | 2012-11-14 | 中国海洋石油总公司 | Liquid high-temperature resistant declining agent for well cementation and preparation method thereof |
CN102775972B (en) * | 2012-07-16 | 2014-12-10 | 中国海洋石油总公司 | Liquid high-temperature resistant declining agent for well cementation and preparation method thereof |
CN105255462A (en) * | 2015-09-02 | 2016-01-20 | 南京云越新材料科技有限公司 | Liquid silicon and preparation method thereof |
CN105255462B (en) * | 2015-09-02 | 2019-02-12 | 南京云越新材料科技有限公司 | A kind of liquid silicon and preparation method thereof |
WO2018052307A1 (en) * | 2016-09-13 | 2018-03-22 | Elkem As | Microsilica slurry and method for producing such slurry |
US11021399B2 (en) | 2019-01-23 | 2021-06-01 | United States Gypsum Company | Self-consolidating geopolymer compositions and methods for making same |
CN110467384A (en) * | 2019-09-10 | 2019-11-19 | 宋文奇 | A kind of light-high-strength concrete and preparation method thereof |
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BR112012030670A2 (en) | 2017-12-05 |
NO20101066A1 (en) | 2012-01-27 |
EA022621B1 (en) | 2016-02-29 |
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NO334511B1 (en) | 2014-03-24 |
MX340657B (en) | 2016-07-20 |
CA2802512A1 (en) | 2012-02-02 |
EA201390164A1 (en) | 2013-05-30 |
US8585819B2 (en) | 2013-11-19 |
DK2598457T3 (en) | 2016-05-17 |
ES2566955T3 (en) | 2016-04-18 |
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BR112012030670B1 (en) | 2020-03-24 |
CA2802512C (en) | 2014-10-14 |
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US20130118383A1 (en) | 2013-05-16 |
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